Page 122 - Advances in bioenergy (2016)
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Table 4.1 Products Yield and Oil Properties from Biomass Catalytic Pyrolysis
Catalyst Silica Sand ZSM-5 FCC
Product yields (wt% on dry biomass)
Organic bio-oil 44.0 32.0 18.2
Water 19.4 30.5 30.4
Coke + Char 8.2 11.1 23.0
CO 13.3 14.6 14.7
CO 2 12.7 9.6 11.9
Other gases (HC) 2.4 2.2 1.8
Elemental analysis of organic bio-oil (wt% )
C 60.5 68.8 64.0
H 7.0 6.7 7.5
O 32.5 24.5 28.5
Organic bio-oil Properties
TAN 93.4 58.2 54.6
HHV (Mj/kg) 19.9 33.2 30.3
In the past few years, CPERI did a systematic study on catalytic pyrolysis. In particular, CPERI
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studied the catalytic biomass pyrolysis in small scale, 38-42 in a modified FCC unit, in an
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once-through transported unit and, recently, in a fully CFB pilot plant (Figure 4.1). CPERI
has tested different acidic materials in this CFB pilot plant unit in order to determine the effect
of heterogeneous catalysis on product yields and quality. Table 4.1 presents the product yields
obtained by catalytic pyrolysis (using a commercially diluted ZSM-5 and an FCC catalyst) and
by thermal pyrolysis (using silica sand as heat carrier). Both catalysts gave lower oil yields
with higher H O, coke, and gas yields. However, the quality of the bio-oil (Table 4.1) was
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better during the catalytic tests, as both catalysts decreased the oxygen content and the TAN,
whereas they also increased the HHV. From Table 4.1 it is clear that H O and CO were the
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main deoxygenation products. The ZSM-5 catalysts produced the best bio-oils with significant
yields (about 30 wt%) and the lowest oxygen content. The two-dimension channel-like pores
of the ZSM-5 were responsible for the low coke yields, which in turn facilitated that the
carbon of the biomass would end up in the liquid product, which was originally the main
target. In contrast with this, the USY zeolite achieved lower deoxygenation, leading to the
lowest organic oil yield. This was attributed mainly to the fact that the USY catalyst produces
higher coke yields; therefore, a significant portion of the biomass’ carbon is lost to solid by-
products (Table 4.1).
CONCLUSIONS

